JPS61180805A - Method of controlling coordination of boiler-steam temperature - Google Patents

Method of controlling coordination of boiler-steam temperature

Info

Publication number
JPS61180805A
JPS61180805A JP1855485A JP1855485A JPS61180805A JP S61180805 A JPS61180805 A JP S61180805A JP 1855485 A JP1855485 A JP 1855485A JP 1855485 A JP1855485 A JP 1855485A JP S61180805 A JPS61180805 A JP S61180805A
Authority
JP
Japan
Prior art keywords
water injection
control
steam temperature
steam
amount
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP1855485A
Other languages
Japanese (ja)
Inventor
物江 利江
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP1855485A priority Critical patent/JPS61180805A/en
Publication of JPS61180805A publication Critical patent/JPS61180805A/en
Pending legal-status Critical Current

Links

Landscapes

  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明は、注水減温器によるボイラ蒸気温度制御に係り
、特に、注水による蒸気流量変動とユニット出力制御と
の相互干渉を抑制する協調制御を行ない、蒸気温度の制
御性向上を可能にするプラント自動制御装置に関する。
[Detailed Description of the Invention] [Field of Application of the Invention] The present invention relates to boiler steam temperature control using a water injection desuperheater, and particularly to cooperative control that suppresses mutual interference between steam flow rate fluctuations due to water injection and unit output control. The present invention relates to an automatic plant control device that enables improved controllability of steam temperature.

〔発明の背景〕[Background of the invention]

発電プラントの制御性は蒸気温度の制御性に左右される
。蒸気温度は過熱器メタルの熱伝達遅れと容量効果を伴
い、大きな時定数とむだ時間のため制御しにくい。
The controllability of power plants depends on the controllability of steam temperature. Steam temperature is difficult to control due to large time constants and dead times, accompanied by heat transfer delays and capacity effects in the superheater metal.

第3図は、ドラムボイラの蒸気温度とタービン出力制御
の代表的な制御系統図である。ドラム1で発生した蒸気
は一次過熱器2及び二次過熱器4で過熱され、例えば、
特公昭54−24681号公報のようにして注水減温器
3で主蒸気温度5が設定値6になるように調節器7によ
り減温水8を注水弁9で注水制御を行なっている。ユニ
ット出力制御は発電量10が要求値11になるように調
節器12で加減弁13を調節してタービン14の出力制
御を行なっている。第4図に注水制御の特性を示す。
FIG. 3 is a typical control system diagram for controlling the steam temperature and turbine output of the drum boiler. The steam generated in the drum 1 is superheated in a primary superheater 2 and a secondary superheater 4, for example,
As disclosed in Japanese Patent Publication No. 54-24681, the water injection control is performed such that deheated water 8 is injected by the regulator 7 and the water injection valve 9 so that the main steam temperature 5 becomes the set value 6 in the water injection desuperheater 3. The unit output control is performed by controlling the output of the turbine 14 by adjusting the control valve 13 with the regulator 12 so that the amount of power generation 10 becomes the required value 11. Figure 4 shows the characteristics of water injection control.

タービン入口蒸気流量W3はユニット出力に見合った量
に制御されるため、注水量W2の変化分は、ドラムより
の蒸気量W1に吸収されるため、負荷変化時の特性は破
線で示すようになる。特に、2での煙道ガスよりの伝熱
量はメタル保有熱量のため、Wlが減少するとWlのエ
ンタルピ11が増加する傾向となる。流体のエンタルピ
を11〜i3とすると、注水による減温特性は次のよう
に示される。
Since the turbine inlet steam flow rate W3 is controlled to an amount commensurate with the unit output, changes in the water injection amount W2 are absorbed by the steam amount W1 from the drum, so the characteristics when the load changes are as shown by the broken line. . In particular, the amount of heat transferred from the flue gas at 2 is the amount of heat held by the metal, so when Wl decreases, the enthalpy 11 of Wl tends to increase. When the enthalpy of the fluid is 11 to i3, the temperature reduction characteristics due to water injection are shown as follows.

W11□+W、i、=Wっi。W11□+W,i,=Wi.

W1+W、=W、より Wz/Ws= (111a)/ (it  lx)とな
る。
Since W1+W,=W, Wz/Ws= (111a)/(it lx).

1t−i3>>iニー12となるため、11の変動に対
してはW、 / W、申K(xl xa)のように示さ
れる。この特性より、W、/W、の少ない時には問題は
ないが、大きいプラントの場合には、早い注水制御を行
なうと注水量の変動を大きくする欠点が生じていた。
Since 1t-i3>>i knee 12, the variation of 11 is expressed as W, /W, ShinK(xl xa). Based on this characteristic, there is no problem when W, /W is small, but in the case of a large plant, if early water injection control is performed, there is a drawback that the fluctuation in the amount of water injection becomes large.

〔発明の目的〕[Purpose of the invention]

本発明の目的は、注水減温による蒸気温度制御において
、ユニット出力制御との干渉を抑制して蒸気温度の制御
性を向上し、プラントの制御性の向上を可能にするボイ
ラ自動制御装置を提供することにある。
An object of the present invention is to provide a boiler automatic control device that improves controllability of steam temperature by suppressing interference with unit output control in steam temperature control by cooling water injection, thereby improving plant controllability. It's about doing.

〔発明の概要〕[Summary of the invention]

本発明の要点は、減温器出口蒸気量を注水量変化時にの
み、ユニット出力制御の許容範囲内で変動させて、減温
器入口蒸気量変動を抑制して、減温効果の向上を図り、
早い注水制御を可能として蒸気温度の制御性の向上を図
ることにある。
The key point of the present invention is to vary the steam volume at the desuperheater outlet within the allowable range of unit output control only when the amount of water injected changes, thereby suppressing fluctuations in the steam volume at the desuperheater inlet, thereby improving the temperature reduction effect. ,
The purpose is to improve controllability of steam temperature by enabling quick water injection control.

(発明の実施例〕 以下、本発明の一実施例を第1図及び第2図を用いて説
明する。
(Embodiment of the Invention) An embodiment of the present invention will be described below with reference to FIGS. 1 and 2.

第1図において注水量を流量検出器15で検出し、微分
器16で変化量を算出し、信号遅れ器17で位相を調整
して、信号制限器18でユニットマスク許容修正量を作
り、出力制御装置の要求量に加えたところが一実施した
部分である。この実施による効果を第2図に示す、特に
、Wlの変動が抑制されているため、W2の変動が少な
くなっていることと、W、の増加により、蒸気により持
ち去られる熱量が増加するため、減温効果が向上し、注
水制御とユニット出力制御との干渉が抑制されているた
め、注水制御を向上させる事ができ、蒸気温度の制御性
の向上と、プラント制御性の向上の効果がある。
In Fig. 1, the amount of water injected is detected by the flow rate detector 15, the amount of change is calculated by the differentiator 16, the phase is adjusted by the signal delayer 17, the unit mask allowable correction amount is created by the signal limiter 18, and the output is This is the part that has been implemented in addition to the amount required by the control device. The effects of this implementation are shown in Figure 2. In particular, since the fluctuations in Wl are suppressed, the fluctuations in W2 are reduced, and as W increases, the amount of heat carried away by the steam increases. Since the temperature reduction effect is improved and interference between water injection control and unit output control is suppressed, water injection control can be improved, which has the effect of improving steam temperature controllability and plant controllability. .

〔発明の効果〕〔Effect of the invention〕

本発明によれば、注水による減温効果以外に。 According to the present invention, in addition to the temperature reduction effect due to water injection.

蒸気流量増加による減温効果と、さらに、注水制御を高
める事が可能のため、蒸気温度制御の向上とプラントの
制御性の向上と、注水量も減少するため、中間負荷運用
プラントの場合には、プラント効率の向上も可能となる
In addition to the temperature reduction effect due to the increased steam flow rate, it is also possible to improve water injection control, which improves steam temperature control, improves plant controllability, and reduces the amount of water injection. , it is also possible to improve plant efficiency.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の一実施例の概略系統図、第2図は本発
明の一実施例の注水、蒸気量と蒸気温度の特性図、第3
図は従来の系統図、第4図は従来の特性図である。 15・・・流量検出器、16・・・微分器、17・・・
信号遅れ器、18・・・信号制限器。 代理人 弁理士 小川勝男 :・ も17 も2Z
Fig. 1 is a schematic system diagram of an embodiment of the present invention, Fig. 2 is a characteristic diagram of water injection, steam amount and steam temperature of an embodiment of the present invention, and Fig. 3
The figure is a conventional system diagram, and FIG. 4 is a conventional characteristic diagram. 15...Flow rate detector, 16...Differentiator, 17...
Signal delay device, 18... signal limiter. Agent: Patent attorney Katsuo Ogawa: Mo17 Mo2Z

Claims (1)

【特許請求の範囲】[Claims] 1、発電プラントに於いて、注水減温装置により蒸気温
度を制御する場合、ユニツトの出力制御によるタービン
加減弁操作に注水制御による注水量変化によるユニツト
出力補正を付加して、前記ユニツトの出力制御による注
水減温制御への干渉を抑制することを特徴とするボイラ
蒸気温度の協調制御方法。
1. In a power generation plant, when the steam temperature is controlled by a water injection cooling device, the output of the unit is controlled by adding a unit output correction based on the water injection amount change due to the water injection control to the turbine control valve operation based on the output control of the unit. A method for cooperatively controlling boiler steam temperature characterized by suppressing interference with water injection temperature reduction control by
JP1855485A 1985-02-04 1985-02-04 Method of controlling coordination of boiler-steam temperature Pending JPS61180805A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1855485A JPS61180805A (en) 1985-02-04 1985-02-04 Method of controlling coordination of boiler-steam temperature

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1855485A JPS61180805A (en) 1985-02-04 1985-02-04 Method of controlling coordination of boiler-steam temperature

Publications (1)

Publication Number Publication Date
JPS61180805A true JPS61180805A (en) 1986-08-13

Family

ID=11974844

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1855485A Pending JPS61180805A (en) 1985-02-04 1985-02-04 Method of controlling coordination of boiler-steam temperature

Country Status (1)

Country Link
JP (1) JPS61180805A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5081451A (en) * 1988-10-20 1992-01-14 Diesel Kiki Co., Ltd. Display system for use in vehicle
CN101988697A (en) * 2009-08-07 2011-03-23 华东电力试验研究院有限公司 Intelligent coordinated control method for thermal power unit
CN105114141A (en) * 2015-09-18 2015-12-02 广东电网有限责任公司电力科学研究院 Unit plant coordinative control method and system
CN105180136A (en) * 2015-10-08 2015-12-23 南京信息工程大学 Thermal-power-plant boiler main steam temperature control method based on fractional order proportional-integral (PI) dynamic matrix
CN105402713A (en) * 2015-12-29 2016-03-16 神华集团有限责任公司 Control method, equipment and system for boiler-turbine coordinated system

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5081451A (en) * 1988-10-20 1992-01-14 Diesel Kiki Co., Ltd. Display system for use in vehicle
CN101988697A (en) * 2009-08-07 2011-03-23 华东电力试验研究院有限公司 Intelligent coordinated control method for thermal power unit
CN105114141A (en) * 2015-09-18 2015-12-02 广东电网有限责任公司电力科学研究院 Unit plant coordinative control method and system
CN105180136A (en) * 2015-10-08 2015-12-23 南京信息工程大学 Thermal-power-plant boiler main steam temperature control method based on fractional order proportional-integral (PI) dynamic matrix
CN105402713A (en) * 2015-12-29 2016-03-16 神华集团有限责任公司 Control method, equipment and system for boiler-turbine coordinated system

Similar Documents

Publication Publication Date Title
JPH0227122Y2 (en)
JPS6239648B2 (en)
JPS61180805A (en) Method of controlling coordination of boiler-steam temperature
JP3285946B2 (en) Steam temperature controller for variable-pressure once-through boiler
JPS6291703A (en) Steaming preventive device for fuel economizer
JPS61190202A (en) Controller for drum level
JPS639638B2 (en)
JPH031563B2 (en)
JPS61187503A (en) Temperature decreasing controller of turbine gland sealing steam
JPS62218702A (en) Steam temperature controller
JPH0765729B2 (en) Boiler automatic control device
JPS62245009A (en) Automatic controller for boiler
JPH01212802A (en) Steam temperature control device for boiler
JP2642999B2 (en) Load control device for combined cycle plant
JP2528640Y2 (en) Turbine forced cooling control device
JPS6390605A (en) Control device for steam generating plant
JPS63279199A (en) Load follow-up control of boiling water type nuclear power generation plant
JPS5888505A (en) Temperature dropping controller for turbine bypass system
JPS6211283Y2 (en)
JPS63687B2 (en)
JP2645129B2 (en) Condensate recirculation flow control device
JPS58165096A (en) Fbr power plant control device
JPS562405A (en) Load control device
JPH0713526B2 (en) Thermal power plant automatic control device
JPS62162808A (en) Fuel-economizer steaming preventive device for thermal powerboiler system